CN114835380A - Melting production process for inhibiting volatilization of borosilicate glass components - Google Patents
Melting production process for inhibiting volatilization of borosilicate glass components Download PDFInfo
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- 239000005388 borosilicate glass Substances 0.000 title claims abstract description 75
- 238000002844 melting Methods 0.000 title claims abstract description 64
- 230000008018 melting Effects 0.000 title claims abstract description 64
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 28
- 230000002401 inhibitory effect Effects 0.000 title claims abstract description 22
- 239000011521 glass Substances 0.000 claims abstract description 64
- 239000002994 raw material Substances 0.000 claims abstract description 53
- 239000006064 precursor glass Substances 0.000 claims abstract description 42
- 239000000843 powder Substances 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 16
- 238000002156 mixing Methods 0.000 claims abstract description 11
- 238000000137 annealing Methods 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 13
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 12
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000000498 ball milling Methods 0.000 claims description 2
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 1
- 229910052593 corundum Inorganic materials 0.000 claims 1
- 229910001845 yogo sapphire Inorganic materials 0.000 claims 1
- 229910052796 boron Inorganic materials 0.000 abstract description 21
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 abstract description 14
- 238000013461 design Methods 0.000 abstract description 3
- 230000000052 comparative effect Effects 0.000 description 10
- 238000001816 cooling Methods 0.000 description 8
- 238000010309 melting process Methods 0.000 description 7
- 238000010348 incorporation Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 4
- 239000000156 glass melt Substances 0.000 description 4
- 238000004321 preservation Methods 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 239000005347 annealed glass Substances 0.000 description 3
- 239000002419 bulk glass Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 238000009740 moulding (composite fabrication) Methods 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 229910052810 boron oxide Inorganic materials 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- UQGFMSUEHSUPRD-UHFFFAOYSA-N disodium;3,7-dioxido-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane Chemical compound [Na+].[Na+].O1B([O-])OB2OB([O-])OB1O2 UQGFMSUEHSUPRD-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000005304 optical glass Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 239000013526 supercooled liquid Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B1/00—Preparing the batches
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/02—Pretreated ingredients
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
- C03C3/089—Glass compositions containing silica with 40% to 90% silica, by weight containing boron
- C03C3/091—Glass compositions containing silica with 40% to 90% silica, by weight containing boron containing aluminium
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
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- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
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Abstract
本发明提供一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺。本发明工艺包括步骤:将硼硅酸盐玻璃中易于挥发的成分所对应的原料粉末熔制成前驱玻璃;然后将前驱玻璃与剩余硼硅酸盐玻璃原料粉末混合熔制即得硼硅酸盐玻璃。本发明采用二次熔制法,将硼硅酸盐玻璃配方中易挥发的组分单独熔制成玻璃,再以玻璃的形式引入到硼硅酸盐玻璃原料中,以玻璃形式代替原配方中原料粉末,使得硼等元素的挥发率大大降低,保证了玻璃设计组分稳定性和生产工艺稳定性,提高了玻璃的均匀性、性能和质量等。The invention provides a melting production process for inhibiting the volatilization of borosilicate glass components. The process of the invention comprises the steps of: melting the raw material powder corresponding to the easily volatile components in the borosilicate glass to form a precursor glass; then mixing and melting the precursor glass and the remaining borosilicate glass raw material powder to obtain the borosilicate glass Glass. The present invention adopts the secondary melting method to separately melt the volatile components in the borosilicate glass formula into glass, and then introduce it into the borosilicate glass raw material in the form of glass, and replace the original formula with the form of glass The raw material powder greatly reduces the volatilization rate of elements such as boron, ensures the stability of the glass design components and the production process, and improves the uniformity, performance and quality of the glass.
Description
技术领域technical field
本发明属于玻璃熔制技术领域,涉及一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺。The invention belongs to the technical field of glass melting, and relates to a melting production process for inhibiting the volatilization of borosilicate glass components.
背景技术Background technique
目前大气污染仍为全世界最严峻的环保问题,其中玻璃行业炉窑燃烧排放的烟雾是环境污染的源头之一,持续影响人类的生存环境。减少玻璃窑炉燃烧排放的途径之一就是减少原料挥发,提高工业生产效率。At present, air pollution is still the most serious environmental protection problem in the world. Among them, the smog emitted by furnaces in the glass industry is one of the sources of environmental pollution, which continues to affect the living environment of human beings. One of the ways to reduce the combustion emissions of glass furnaces is to reduce the volatilization of raw materials and improve the efficiency of industrial production.
硼硅酸盐玻璃是一种低成本材料,它广泛应用于仪器玻璃、日用玻璃、光学玻璃、防火玻璃等领域,这也是得益于硼硅酸盐玻璃许多优异的性能,如:良好的化学稳定性、热稳定性、机械性能、光学性能,低损耗率等。然而,硼硅酸盐玻璃需要较高的熔制温度,一些氧化物易挥发,导致了硼硅酸盐玻璃的成分和性能都会发生变化,如粘度、密度、液相线温度和折射率等。B2O3作为硼硅酸盐玻璃的重要形成体氧化物,其挥发较为严重。据报道,B2O3单独熔制玻璃的质量损失可达到20%,而且当原料中水分含量更高时其挥发率也会急剧增加,因此国外一些厂家在生产硼玻璃时通常以无水硼酸或者无水硼砂引入B2O3,但这也仅能降低小部分的氧化硼挥发,是微乎其微的。B2O3的挥发会出现玻璃局部高硅的现象,降低玻璃的均匀性,直接影响玻璃结构、性能、质量。玻璃作为一种各向同性的过冷液体,玻璃的均匀性决定了其性能。因此如何降低硼等元素的挥发,降低生产成本,提高玻璃的均匀性、性能和质量等,成为了玻璃工业关注的重点。Borosilicate glass is a low-cost material, it is widely used in instrument glass, daily glass, optical glass, fireproof glass and other fields, which is also due to the many excellent properties of borosilicate glass, such as: good Chemical stability, thermal stability, mechanical properties, optical properties, low loss rate, etc. However, borosilicate glass requires a higher melting temperature, and some oxides are volatile, resulting in changes in the composition and properties of borosilicate glass, such as viscosity, density, liquidus temperature, and refractive index. As an important former oxide of borosilicate glass, B 2 O 3 has serious volatilization. According to reports, the mass loss of B 2 O 3 melting glass alone can reach 20%, and its volatilization rate will increase sharply when the moisture content in the raw material is higher, so some foreign manufacturers usually use anhydrous boric acid when producing boron glass. Or anhydrous borax can be introduced into B 2 O 3 , but this can only reduce the volatilization of a small part of boron oxide, which is very small. The volatilization of B 2 O 3 will cause the phenomenon of local high silicon content in the glass, reduce the uniformity of the glass, and directly affect the structure, performance and quality of the glass. As an isotropic supercooled liquid, the uniformity of glass determines its performance. Therefore, how to reduce the volatilization of elements such as boron, reduce production costs, and improve the uniformity, performance and quality of glass, has become the focus of the glass industry.
现有技术中已有关于降低硼挥发的报道,但大多都是改进玻璃窑炉结构来降低硼挥发。如中国专利文献CN107188393A公开了一种控制硼硅酸盐单片防火玻璃生产中硼挥发的熔窑装置,该发明采用预熔区全电熔熔化和强熔区火焰加电助熔的熔化方式,可以减少硼硅酸盐单片防火玻璃生产中硼的挥发,最大可减少硼挥发5%~15%。该发明通过改进玻璃窑炉结构来降低硼挥发,不能从根本上即工艺本身解决硼挥发的问题,且对于降低硼挥发的效果欠佳。There are reports on reducing boron volatilization in the prior art, but most of them are to improve the structure of the glass furnace to reduce boron volatilization. For example, Chinese patent document CN107188393A discloses a melting furnace device for controlling the volatilization of boron in the production of borosilicate monolithic fireproof glass. It can reduce the volatilization of boron in the production of borosilicate monolithic fireproof glass, and can reduce the volatilization of boron by 5% to 15% at most. The invention reduces the volatilization of boron by improving the structure of the glass furnace, cannot fundamentally solve the problem of volatilization of boron by the process itself, and is not effective in reducing the volatilization of boron.
因此,探究一种从工艺本身降低硼等元素的挥发,降低生产成本,提高玻璃的均匀性、性能和质量等工艺方法,值得进一步研究。Therefore, it is worth further research to explore a process method to reduce the volatilization of elements such as boron, reduce production costs, and improve the uniformity, performance and quality of glass from the process itself.
发明内容SUMMARY OF THE INVENTION
针对现有技术存在的不足,本发明提供一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺。本发明主要解决了目前通过传统熔融法制备玻璃存在的缺陷:一些元素(例如B、Na等元素)挥发后玻璃成分改变、玻璃性质不均匀性、玻璃质量和性能降低等问题。本发明采用二次熔制法,将硼硅酸盐玻璃配方中易挥发的组分单独熔制成玻璃,再以玻璃的形式引入到硼硅酸盐玻璃原料中,以玻璃形式代替原配方中原料粉末,使得硼等元素的挥发率大大降低,保证了玻璃设计组分稳定性和生产工艺稳定性,提高了玻璃的均匀性、性能和质量等。Aiming at the deficiencies in the prior art, the present invention provides a melting production process for inhibiting the volatilization of borosilicate glass components. The invention mainly solves the defects existing in glass preparation by traditional melting method: the glass composition changes after volatilization of some elements (such as B, Na, etc.), the inhomogeneity of glass properties, and the reduction of glass quality and performance. The present invention adopts a secondary melting method, and the volatile components in the borosilicate glass formula are separately melted into glass, which is then introduced into the borosilicate glass raw material in the form of glass, and the original formula is replaced by the form of glass. The raw material powder greatly reduces the volatilization rate of elements such as boron, ensures the stability of the glass design components and the production process, and improves the uniformity, performance and quality of the glass.
本发明的技术方案如下:The technical scheme of the present invention is as follows:
一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺,包括步骤:A melting production process for inhibiting the volatilization of borosilicate glass components, comprising the steps of:
(1)将硼硅酸盐玻璃中易于挥发的成分所对应的原料粉末熔制成前驱玻璃;(1) The raw material powder corresponding to the easily volatile components in the borosilicate glass is melted into the precursor glass;
(2)然后将前驱玻璃与剩余硼硅酸盐玻璃原料粉末混合熔制即得硼硅酸盐玻璃。(2) Then, the precursor glass and the remaining borosilicate glass raw material powder are mixed and melted to obtain borosilicate glass.
根据本发明优选的,步骤(1)中,所述硼硅酸盐玻璃包括如下质量百分比的成分组成:SiO2 60-85%,B2O3 5-17%,Na2O+K2O 4-15%,CaO 0.5-5%,Al2O3 2-10%。Preferably according to the present invention, in step (1), the borosilicate glass comprises the following components by mass percentage: SiO 2 60-85%, B 2 O 3 5-17%, Na 2 O+K 2 O 4-15%, CaO 0.5-5%, Al 2 O 3 2-10%.
优选的,所述硼硅酸盐玻璃包括如下原料制备得到:SiO2、B2O3、K2CO3、Na2CO3、CaCO3、Al2O3。Preferably, the borosilicate glass is prepared from the following raw materials: SiO 2 , B 2 O 3 , K 2 CO 3 , Na 2 CO 3 , CaCO 3 , and Al 2 O 3 .
优选的,硼硅酸盐玻璃中易于挥发的成分所对应的原料为B2O3、Na2CO3。Preferably, the raw materials corresponding to the easily volatile components in the borosilicate glass are B 2 O 3 and Na 2 CO 3 .
根据本发明优选的,步骤(1)中,前驱玻璃的制备方法包括步骤:将硼硅酸盐玻璃中易于挥发的成分所对应的原料粉末混合、熔融,冷却成型后,经退火处理、制成碎块得到前驱玻璃。Preferably according to the present invention, in step (1), the preparation method of the precursor glass includes the steps of: mixing and melting the raw material powder corresponding to the easily volatile components in the borosilicate glass, cooling and forming, annealing and forming Shards get precursor glass.
优选的,混合方法为室温球磨混合3-5h。Preferably, the mixing method is room temperature ball milling for 3-5 hours.
优选的,熔融温度为900-1100℃,优选为1000℃;熔融保温时间为20-40min,优选为30min;熔融升温速率为3-8℃/min;退火处理温度为300-500℃,优选为400℃;退火处理时间为1-3h,优选为2h。本发明进行退火处理从而消除内应力。Preferably, the melting temperature is 900-1100°C, preferably 1000°C; the melting and holding time is 20-40min, preferably 30min; the melting temperature rise rate is 3-8°C/min; the annealing temperature is 300-500°C, preferably 400°C; annealing treatment time is 1-3h, preferably 2h. The present invention performs annealing treatment to relieve internal stress.
优选的,所述前驱玻璃是尺寸为0.5-1cm的块体。Preferably, the precursor glass is a block with a size of 0.5-1 cm.
根据本发明优选的,步骤(1)中,将硼硅酸盐玻璃中易于挥发的成分所对应的原料粉末混合均匀后,取所得粉末总质量的50%-100%熔制成前驱玻璃。剩余易于挥发的成分所对应的原料以粉末形式加入,继而进行后续混合熔制。优选的,将硼硅酸盐玻璃中易于挥发的成分所对应的全部原料粉末熔制成前驱玻璃。Preferably according to the present invention, in step (1), after uniformly mixing the raw material powders corresponding to the easily volatile components in the borosilicate glass, 50%-100% of the total mass of the obtained powders is melted into the precursor glass. The raw materials corresponding to the remaining volatile components are added in the form of powder, followed by subsequent mixing and melting. Preferably, all the raw material powders corresponding to the easily volatile components in the borosilicate glass are melted to form the precursor glass.
根据本发明优选的,步骤(2)中,硼硅酸盐玻璃的制备方法包括步骤:将前驱玻璃与剩余硼硅酸盐玻璃原料粉末混合熔融,冷却成型后,经退火处理即得硼硅酸盐玻璃。Preferably according to the present invention, in step (2), the preparation method of borosilicate glass includes the steps of: mixing and melting the precursor glass and remaining borosilicate glass raw material powder, cooling and forming, and annealing to obtain borosilicate glass Salt glass.
优选的,熔融温度不超过1580℃,优选为1580℃;熔融保温时间为1-3h,优选为1.5h;熔融升温速率为3-8℃/min;退火处理温度为300-600℃,优选为530℃,退火处理时间为1-3h,优选为2h。Preferably, the melting temperature does not exceed 1580°C, preferably 1580°C; the melting and holding time is 1-3h, preferably 1.5h; the melting temperature rise rate is 3-8°C/min; the annealing temperature is 300-600°C, preferably 530℃, the annealing treatment time is 1-3h, preferably 2h.
本发明的技术特点及有益效果如下:The technical characteristics and beneficial effects of the present invention are as follows:
1、本发明采用二次熔制法,将硼硅酸盐玻璃配方中易挥发的组分单独熔制成玻璃,再以玻璃的形式引入到硼硅酸盐玻璃原料中,以玻璃形式代替原配方中原料粉末,使得硼等元素的挥发率大大降低,保证了玻璃设计组分稳定性和生产工艺稳定性,提高了玻璃的均匀性、性能和质量等。1. The present invention adopts a secondary melting method, and the volatile components in the borosilicate glass formula are separately melted into glass, and then introduced into the borosilicate glass raw material in the form of glass, and the original glass is replaced by the form of glass. The raw material powder in the formula greatly reduces the volatilization rate of elements such as boron, ensures the stability of the glass design components and the production process, and improves the uniformity, performance and quality of the glass.
2、本发明熔制方法具有更低的损失率,降低了易挥发成分的散失和能量损耗,有效的提高了能源利用效率,提高了工业生产效率。2. The melting method of the present invention has a lower loss rate, reduces the loss of volatile components and energy loss, effectively improves energy utilization efficiency, and improves industrial production efficiency.
3、本发明节约了原料资源的消耗,引入的前驱玻璃碎块作为助熔剂,有助于玻璃液澄清均化。本发明生产工艺熔制的硼硅酸盐玻璃具有优异的均匀性,其中气泡条纹明显有所减少;良好的均匀性保证了玻璃性能的稳定性,提高了玻璃的使用可靠性;所得玻璃的性能和质量较高。3. The present invention saves the consumption of raw material resources, and the introduced precursor glass fragments are used as a fluxing agent, which is helpful for the clarification and homogenization of the glass liquid. The borosilicate glass melted by the production process of the invention has excellent uniformity, wherein the bubble streaks are obviously reduced; the good uniformity ensures the stability of the glass performance and improves the use reliability of the glass; the properties of the obtained glass are and higher quality.
4、本发明具有生产工艺简单,易操作,成本低等优点。4. The invention has the advantages of simple production process, easy operation and low cost.
5、本发明特定尺寸的前驱玻璃利于其与剩余原料混合均匀,从而利于保证硼硅酸盐玻璃的均匀性。5. The specific size of the precursor glass of the present invention is favorable for mixing it with the remaining raw materials uniformly, thereby helping to ensure the uniformity of the borosilicate glass.
附图说明:Description of drawings:
图1为本发明实施例和对比例得到的Glass0、20、50、100的X射线衍射(XRD)图谱。Fig. 1 is the X-ray diffraction (XRD) patterns of Glass0, 20, 50, 100 obtained in the embodiment of the present invention and the comparative example.
图2为本发明实施例和对比例得到的Glass0、20、50、100的扫描电镜(SEM)图像。FIG. 2 is the scanning electron microscope (SEM) images of Glass0, 20, 50, and 100 obtained in the embodiment of the present invention and the comparative example.
图3为本发明对比例1得到的Glass0的X射线(EDS)能谱。FIG. 3 is the X-ray (EDS) energy spectrum of Glass0 obtained in Comparative Example 1 of the present invention.
图4为本发明实施例1得到的Glass100的X射线(EDS)能谱。FIG. 4 is the X-ray (EDS) energy spectrum of Glass100 obtained in Example 1 of the present invention.
具体实施方式Detailed ways
下面通过具体实施例并结合附图对本发明作进一步说明,但不限于此。The present invention will be further described below through specific embodiments and in conjunction with the accompanying drawings, but is not limited thereto.
实施例中所用原料如无特殊说明,均为99.99%纯度的化学试剂,市购产品。The raw materials used in the examples are all chemical reagents with a purity of 99.99%, commercially available products unless otherwise specified.
实施例1Example 1
一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺,所述硼硅酸盐玻璃包括如下质量百分比的成分组成:SiO2 68%,B2O3 13%,Na2O 10%,K2O 2%,CaO 2%,Al2O3 5%。所用原料为:SiO2、B2O3、Na2CO3、K2CO3、CaCO3、Al2O3。A melting production process for inhibiting the volatilization of borosilicate glass components, the borosilicate glass includes the following components by mass percentage: SiO 2 68%, B 2 O 3 13%, Na 2 O 10%, K 2 O 2%,
制备包括步骤如下:The preparation includes the following steps:
(1)前驱玻璃的制备:按上述成分比例换算原料用量,分别称取B2O3、Na2CO3,放置球磨机上室温均匀混合4h,将原料放置马弗炉中加热至1000℃熔制成玻璃熔体,熔融升温速率为5℃/min,熔融保温时间为30min,将熔体快速倒至铜板上冷却成型得到块状玻璃。再将成型后的块状玻璃进行400℃退火处理2h,以此消除内应力。将退火后玻璃制成尺寸为0.5-1cm无规则的块体,得到前驱玻璃。(1) Preparation of precursor glass: convert the amount of raw materials according to the above component ratios, weigh B 2 O 3 and Na 2 CO 3 respectively, place them on a ball mill and mix them evenly at room temperature for 4 hours, and place the raw materials in a muffle furnace and heat to 1000 ℃ for melting A glass melt is formed, the melting heating rate is 5°C/min, the melting holding time is 30 min, and the melt is quickly poured onto a copper plate for cooling and forming to obtain a block glass. The formed bulk glass is then annealed at 400°C for 2 hours to eliminate internal stress. The annealed glass is made into a random block with a size of 0.5-1 cm to obtain a precursor glass.
(2)按上述成分比例换算原料用量,将步骤(1)制备的前驱玻璃与剩余原料混合均匀,加热至1580℃熔融保温1.5h,熔融升温速率为5℃/min,冷却成型后,530℃退火处理2h即得硼硅酸盐玻璃,记为Glass100。(2) Convert the amount of raw materials according to the above component ratio, mix the precursor glass prepared in step (1) and the remaining raw materials evenly, heat to 1580 ° C for melting and heat preservation for 1.5 h, the melting temperature rise rate is 5 ° C/min, after cooling and forming, 530 ° C After annealing for 2h, borosilicate glass was obtained, which was recorded as Glass100.
根据熔制的前后质量变化,得出硼硅酸盐玻璃Glass100的损失量仅有5.08g,挥发率为4.74%。这说明在熔融过程中掺入前驱玻璃块体对一些原料的挥发起到了有效抑制作用。其中,挥发率计算公式如下:According to the quality change before and after melting, it is concluded that the loss of borosilicate glass Glass100 is only 5.08g, and the volatilization rate is 4.74%. This shows that the incorporation of precursor glass blocks during the melting process can effectively inhibit the volatilization of some raw materials. Among them, the calculation formula of the volatilization rate is as follows:
实施例2Example 2
一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺,所述硼硅酸盐玻璃包括如下质量百分比的成分组成:SiO2 68%,B2O3 13%,Na2O 10%,K2O 2%,CaO 2%,Al2O3 5%。所用原料为:SiO2、B2O3、Na2CO3、K2CO3、CaCO3、Al2O3。A melting production process for inhibiting the volatilization of borosilicate glass components, the borosilicate glass includes the following components by mass percentage: SiO 2 68%, B 2 O 3 13%, Na 2 O 10%, K 2 O 2%,
制备包括步骤如下:The preparation includes the following steps:
(1)前驱玻璃的制备:按上述成分比例换算原料用量,分别称取B2O3、Na2CO3,放置球磨机上室温均匀混合4h;将所得粉末总质量的50%放置马弗炉中加热至1000℃熔制成玻璃熔体,熔融升温速率为5℃/min,熔融保温时间为30min,将熔体快速倒至铜板上冷却成型得到块状玻璃。再将成型后的块状玻璃进行400℃退火处理2h,以此消除内应力。将退火后玻璃制成尺寸为0.5-1cm无规则的块体,得到前驱玻璃。(1) Preparation of precursor glass: convert the amount of raw materials according to the above component ratios, weigh B 2 O 3 and Na 2 CO 3 respectively, and place them on a ball mill for uniform mixing at room temperature for 4 hours; 50% of the total mass of the obtained powder is placed in a muffle furnace Heating to 1000°C and melting into glass melt, the melting heating rate is 5°C/min, the melting holding time is 30min, and the melt is quickly poured onto a copper plate for cooling and forming to obtain block glass. The formed bulk glass is then annealed at 400°C for 2 hours to eliminate internal stress. The annealed glass is made into a random block with a size of 0.5-1 cm to obtain a precursor glass.
(2)按上述成分比例换算原料用量,将步骤(1)制备的前驱玻璃、剩余B2O3和Na2CO3的混合粉末、其它原料粉末混合均匀,加热至1580℃熔融保温1.5h,熔融升温速率为5℃/min,冷却成型后,530℃退火处理2h即得硼硅酸盐玻璃,记为Glass50。(2) Convert the amount of raw materials according to the proportion of the above components, mix the precursor glass prepared in step (1), the mixed powder of remaining B 2 O 3 and Na 2 CO 3 , and other raw material powders evenly, and heat to 1580 ° C for melting and heat preservation for 1.5 h, The melting and heating rate was 5°C/min. After cooling and forming, borosilicate glass was obtained by annealing at 530°C for 2 hours, which was recorded as Glass50.
按实施例1的方法计算损失量以及挥发率,得出硼硅酸盐玻璃Glass50的损失量为8.34g,挥发率达到7.79%。这说明在熔融过程中掺入50%前驱玻璃块体对一些原料的挥发起到一定的抑制作用。The loss and volatilization rate were calculated according to the method of Example 1, and it was concluded that the loss of the borosilicate glass Glass50 was 8.34 g, and the volatilization rate reached 7.79%. This shows that the incorporation of 50% of the precursor glass block in the melting process has a certain inhibitory effect on the volatilization of some raw materials.
对比例1Comparative Example 1
一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺,所述硼硅酸盐玻璃包括如下质量百分比的成分组成:SiO2 68%,B2O3 13%,Na2O 10%,K2O 2%,CaO 2%,Al2O3 5%。所用原料为:SiO2、B2O3、Na2CO3、K2CO3、CaCO3、Al2O3。。A melting production process for inhibiting the volatilization of borosilicate glass components, the borosilicate glass includes the following components by mass percentage: SiO 2 68%, B 2 O 3 13%, Na 2 O 10%, K 2 O 2%,
制备包括步骤如下:The preparation includes the following steps:
按上述成分比例换算原料用量,将各原料混合均匀,加热至1580℃熔融保温1.5h,熔融升温速率为5℃/min,冷却成型后,530℃退火处理2h即得硼硅酸盐玻璃,记为Glass0。Calculate the amount of raw materials according to the above component ratios, mix the raw materials evenly, heat to 1580 °C for melting and heat preservation for 1.5 hours, and the melting temperature rise rate is 5 °C/min. for Glass0.
按实施例1的方法计算损失量以及挥发率,得出硼硅酸盐玻璃Glass0的损失量为11.60g,挥发率达到10.83%。这说明熔融过程中原料(Na2O、B2O3等氧化物)的挥发较为严重。The loss and volatilization rate were calculated according to the method of Example 1, and it was concluded that the loss of the borosilicate glass Glass0 was 11.60 g, and the volatilization rate reached 10.83%. This shows that the volatilization of raw materials (oxides such as Na 2 O, B 2 O 3 , etc.) during the melting process is more serious.
对比例2Comparative Example 2
一种抑制硼硅酸盐玻璃成分挥发的熔制生产工艺,所述硼硅酸盐玻璃包括如下质量百分比的成分组成:SiO2 68%,B2O3 13%,Na2O 10%,K2O 2%,CaO 2%,Al2O3 5%。所用原料为:SiO2、B2O3、Na2CO3、K2CO3、CaCO3、Al2O3。A melting production process for inhibiting the volatilization of borosilicate glass components, the borosilicate glass includes the following components by mass percentage: SiO 2 68%, B 2 O 3 13%, Na 2 O 10%, K 2 O 2%,
制备包括步骤如下:The preparation includes the following steps:
(1)前驱玻璃的制备:按上述成分比例换算原料用量,分别称取B2O3、Na2CO3,放置球磨机上室温均匀混合4h;将所得粉末总质量的20%放置马弗炉中加热至1000℃熔制成玻璃熔体,熔融升温速率为5℃/min,熔融保温时间为30min,将熔体快速倒至铜板上冷却成型得到块状玻璃。再将成型后的块状玻璃进行400℃退火处理2h,以此消除内应力。将退火后玻璃制成尺寸为0.5-1cm无规则的块体,得到前驱玻璃。(1) Preparation of precursor glass: convert the amount of raw materials according to the above component ratios, weigh B 2 O 3 and Na 2 CO 3 respectively, and place them on a ball mill for uniform mixing at room temperature for 4 hours; 20% of the total mass of the obtained powder is placed in a muffle furnace Heating to 1000°C and melting into glass melt, the melting heating rate is 5°C/min, the melting holding time is 30min, and the melt is quickly poured onto a copper plate for cooling and forming to obtain block glass. The formed bulk glass is then annealed at 400°C for 2 hours to eliminate internal stress. The annealed glass is made into a random block with a size of 0.5-1 cm to obtain a precursor glass.
(2)按上述成分比例换算原料用量,将步骤(1)制备的前驱玻璃、剩余B2O3和Na2CO3的混合粉末、其它原料粉末混合均匀,加热至1580℃熔融保温1.5h,熔融升温速率为5℃/min,冷却成型后,530℃退火处理2h即得硼硅酸盐玻璃,记为Glass20。(2) Convert the amount of raw materials according to the proportion of the above components, mix the precursor glass prepared in step (1), the mixed powder of remaining B 2 O 3 and Na 2 CO 3 , and other raw material powders evenly, and heat to 1580 ° C for melting and heat preservation for 1.5 h, The melting and heating rate was 5°C/min. After cooling and forming, borosilicate glass was obtained by annealing at 530°C for 2 hours, which was recorded as Glass20.
按实施例1的方法计算损失量以及挥发率,得出硼硅酸盐玻璃Glass20的损失量为10.29g,挥发率达到9.61%。这说明在熔融过程中掺入20%前驱玻璃块体对一些原料的挥发起到一定的抑制作用,但抑制作用较弱。The loss and volatilization rate were calculated according to the method of Example 1, and it was concluded that the loss of the borosilicate glass Glass20 was 10.29 g, and the volatilization rate reached 9.61%. This shows that the incorporation of 20% precursor glass blocks in the melting process has a certain inhibitory effect on the volatilization of some raw materials, but the inhibitory effect is weak.
试验例1Test Example 1
样品挥发率分析Analysis of sample volatilization rate
对实施例以及对比例的制备方法进行挥发率测试。根据熔制前后的质量变化,测试挥发量以及挥发率。结果如表1所示。The volatilization rate test was carried out on the preparation methods of the examples and the comparative examples. According to the mass change before and after melting, the volatilization amount and volatilization rate were tested. The results are shown in Table 1.
表1Table 1
由表1,发现不同比例前驱玻璃的掺入会影响到硼硅酸盐玻璃的损失率。当引入前驱玻璃的比例越大,得到硼硅酸盐玻璃的损失率越低,这意味着前驱玻璃的引入可以大大降低B2O3、Na2CO3的挥发。特别是,原料中B2O3、Na2CO3完全以前驱玻璃的形式引入时,最终得到硼硅酸盐玻璃Glass100的挥发率仅有4.74%。From Table 1, it is found that the incorporation of different proportions of precursor glass will affect the loss rate of borosilicate glass. When the proportion of the precursor glass introduced is larger, the loss rate of the borosilicate glass is lower, which means that the introduction of the precursor glass can greatly reduce the volatilization of B 2 O 3 and Na 2 CO 3 . In particular, when B 2 O 3 and Na 2 CO 3 in the raw materials are completely introduced in the form of precursor glass, the volatilization rate of finally obtained borosilicate glass Glass100 is only 4.74%.
试验例2Test Example 2
晶相分析Crystal phase analysis
将实施例和对比例得到的玻璃样品进行X射线衍射(XRD)分析,如图1所示。The glass samples obtained in the examples and comparative examples were subjected to X-ray diffraction (XRD) analysis, as shown in FIG. 1 .
实施例以及对比例所得玻璃样品均呈现弥散的馒头峰,并无尖锐的衍射峰,说明样品结构中无晶相产生,为无定型状态,这说明熔制的硼硅酸盐玻璃都为纯玻璃。The glass samples obtained in the examples and the comparative examples all show diffuse steamed bread peaks without sharp diffraction peaks, indicating that there is no crystalline phase in the sample structure, and it is in an amorphous state, which indicates that the melted borosilicate glass is pure glass. .
试验例3Test Example 3
样品形貌与成分分析Sample morphology and composition analysis
将实施例以及对比例制备的玻璃样品进行扫描电镜(SEM)测试,如图2所示。The glass samples prepared in the examples and the comparative examples were tested by scanning electron microscope (SEM), as shown in FIG. 2 .
由图2可知,Glass0样品表面呈现凹凸不平,且在表面上存在一些不均匀分布的50-200nm的颗粒。随着前驱玻璃加入量的增加,玻璃表面越平整越均匀。即硼硅酸盐玻璃样品中引入前驱玻璃的比例越大,表面缺陷也越来越少。这说明在原料中引入前驱玻璃块体可以起到降低B2O3、Na2O等氧化物挥发的作用,并有利于玻璃熔制过程中的均匀性。It can be seen from Figure 2 that the surface of the Glass0 sample is uneven, and there are some unevenly distributed particles of 50-200 nm on the surface. With the increase in the amount of the precursor glass added, the glass surface is flatter and more uniform. That is, the greater the proportion of the precursor glass introduced into the borosilicate glass sample, the less surface defects. This shows that the introduction of the precursor glass bulk into the raw material can reduce the volatilization of oxides such as B 2 O 3 and Na 2 O, and is beneficial to the uniformity of the glass melting process.
将实施例以及对比例制备的玻璃样品进行X射线能谱(EDS)测试,如图3、4所示。通过对样品进行线扫描,得到了各个元素在玻璃内部强度含量分布。如图3可知,Glass0的各元素含量波动尤为显著,尤其是K、Al、O、Si元素明显分布不均匀,这说明Glass0原料在熔制过程中挥发造成局部元素富集或缺失,导致成型的玻璃呈现不均匀性。图4中,Glass100的各元素含量变化较小,仅有较小的浮动,这说明掺入前驱玻璃降低了玻璃的挥发率,使得玻璃在熔制过程中更好地均匀熔融,提高了玻璃均匀性。良好的均匀性保证了玻璃性能的稳定性,提高了玻璃的使用可靠性。无论从损失率还是均匀性上,掺入前驱玻璃得到的玻璃均优于未掺入前驱玻璃得到的玻璃。X-ray energy spectroscopy (EDS) tests were performed on the glass samples prepared in the examples and comparative examples, as shown in FIGS. 3 and 4 . Through line scanning of the sample, the distribution of the intensity content of each element in the glass was obtained. As can be seen from Figure 3, the content of each element of Glass0 fluctuates significantly, especially the K, Al, O, Si elements are obviously unevenly distributed, which indicates that the volatilization of Glass0 raw materials during the melting process causes local element enrichment or lack, resulting in molding The glass exhibits inhomogeneity. In Figure 4, the content of each element in Glass100 changes little, with only small fluctuations, which shows that the incorporation of precursor glass reduces the volatilization rate of the glass, which makes the glass melt more uniformly during the melting process, and improves the uniformity of the glass. sex. Good uniformity ensures the stability of glass performance and improves the reliability of glass in use. In terms of loss rate and uniformity, the glass obtained by incorporating the precursor glass is superior to the glass obtained by not incorporating the precursor glass.
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CN104496152A (en) * | 2014-12-03 | 2015-04-08 | 东莞市长安东阳光铝业研发有限公司 | Method for controlling boron volatilization in neutral borosilicate glass melting process |
CN106477877A (en) * | 2016-10-17 | 2017-03-08 | 河北省沙河玻璃技术研究院 | A kind of extra-high refraction high density environment-friendly type cameo glass and preparation method thereof |
CN107188393A (en) * | 2017-07-06 | 2017-09-22 | 中国建材国际工程集团有限公司 | It is a kind of to control the melting furnaces device and method that boron volatilizees in the production of borosilicate single-sheet fire-resistant glass |
CN110272205A (en) * | 2019-06-26 | 2019-09-24 | 醴陵旗滨电子玻璃有限公司 | A kind of borosilicate glass and its preparation method and application |
Cited By (1)
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CN117303733A (en) * | 2023-09-26 | 2023-12-29 | 清远南玻节能新材料有限公司 | Borosilicate glass and preparation method thereof |
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